CN1221719A - Prodn. tech. of disposable multi-element compound fertilizer - Google Patents

Prodn. tech. of disposable multi-element compound fertilizer Download PDF

Info

Publication number
CN1221719A
CN1221719A CN 98114356 CN98114356A CN1221719A CN 1221719 A CN1221719 A CN 1221719A CN 98114356 CN98114356 CN 98114356 CN 98114356 A CN98114356 A CN 98114356A CN 1221719 A CN1221719 A CN 1221719A
Authority
CN
China
Prior art keywords
percent
granulator
compound fertilizer
temperature
liquid ammonia
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN 98114356
Other languages
Chinese (zh)
Other versions
CN1088446C (en
Inventor
王可义
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CANG ANZHI
Original Assignee
CANG ANZHI
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CANG ANZHI filed Critical CANG ANZHI
Priority to CN98114356A priority Critical patent/CN1088446C/en
Publication of CN1221719A publication Critical patent/CN1221719A/en
Application granted granted Critical
Publication of CN1088446C publication Critical patent/CN1088446C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05BPHOSPHATIC FERTILISERS
    • C05B1/00Superphosphates, i.e. fertilisers produced by reacting rock or bone phosphates with sulfuric or phosphoric acid in such amounts and concentrations as to yield solid products directly
    • C05B1/06Ammoniation of superphosphates

Abstract

A one-pass applied multi-elemtn compound fertilizer is prepared from bentone, heavy calcium, potassium chloride and urea through granulating based on the heat from reaction between sulfuric acid and liquefied nitrogen, drying and cooling to obtain compound NPK fertilizer. It features less liquid phases and low viscosity during its preparing process (resulting in easy breaking and granulating), and modification of heavy calcium to reduce crystallized water for higher physical nature.

Description

Production process of disposable multi-element compound fertilizer
The invention relates to a production process of a chlorine-based nitrogen-phosphorus-potassium compound fertilizer, in particular to a production process of a disposable multi-element compound fertilizer which is prepared by taking a phosphorus source, a potassium source, urea and an additive as raw materials.
In the prior art, when the chlorine-based nitrogen-phosphorus-potassium compound fertilizer is produced, free phosphoric acid and monocalcium phosphate contained in the coarse whiting can react with urea to generate urea phosphate and a mixture of monocalcium phosphate and urea, and original crystal water of monocalcium phosphate can be released. The two substances have high solubility and can be dissolved in the water contained in the heavy calcium to increase the liquid phase of the mixture, so that the material becomes sticky and is not beneficial to crushing and granulating, therefore, when the urea-heavy calcium is used for producing the compound fertilizer, theheavy calcium is modified.
The invention aims to provide a production process of a disposable multi-element compound fertilizer, which makes monocalcium phosphate in heavy calcium react with liquid nitrogen to convert dicalcium phosphate and monoammonium phosphate so as to change the physical properties of raw materials and reduce the release of crystal water.
In order to achieve the purpose, the invention adopts the following technical scheme: the invention is a nitrogen-phosphorus-potassium compound fertilizer which is produced by granulating, drying and cooling an additive (bentonite), a phosphorus source (triple superphosphate), a potassium source (potassium chloride) and urea according to a certain proportion on the basis of taking sulfuric acid and liquid ammonia as reaction heat, and is characterized in that:
(1) according to the ratio of bentonite to heavy calcium (P)2O5= 41%: potassium chloride (K)2O =62 percent and urea(= 64%) = 1: 6.43: 2.87: 8.7 (weight ratio) and uniformly mixing;
(2) modifying the coarse whiting by adopting an amino-transfer method, introducing liquid ammonia (containing 82.3 percent of nitrogen) at a raw material inlet of a granulator, adding the liquid ammonia according to 1.35 percent of the amount of a finished product, and carrying out ammoniation treatment on the coarse whiting in the raw material;
(3) heating the materials in the granulating bed layer by adopting ammonia-acid reaction heat, and adding liquid ammonia and sulfuric acid into the granulating section at the same time according to the weight ratio of 1: 2-3.5;
(4) in the reaction process of the ammonia and the acid, the temperature of the material at the outlet of the granulator is ensured to be between 60 and 80 ℃, the PH value is between 5.5 and 7.0, and the water content is less than or equal to 3.0 percent;
(5) the material at the outlet of the granulator is sent into a dryer for drying, the temperature at the inlet of the dryer is between 110 and 165 ℃, and the temperature of the material at the inlet of the dryer is ensured to be between 60 and 70 ℃, and the moisture content is less than or equal to 2.0 percent;
(6) and (3) feeding the material at the outlet of the granulator into a cooling machine for cooling treatment, and ensuring that the temperature of the material is reduced to 35-55 ℃.
The main reaction equation is:
the invention has the positive effects that: the purpose of the sulfuric acid and the liquid ammonia which are put into the production process is that the reaction heat is utilized to heat the materials for granulation, the generated ammonium sulfate is mixed with the phosphoric acid-calcium and then mixed with the urea, the ammonium sulfate reacts with the monocalcium phosphate to generate ammonium gypsum double salt, and the generated ammonium phosphate avoids the degradation of the water-soluble phosphorus pentoxide, so that the mixedmaterials have good physical properties and are easy to granulate.
Example 1:
taking 46 kg of bentonite, 298 kg of heavy calcium, 133 kg of potassium chloride, 403 kg of urea, 47 kg of liquid ammonia and 105 kg of sulfuric acid, and producing the total nutrient (N + P) of the product according to the production process2O5+K2O) is more than or equal to 42 percent, total nitrogen (N) is more than or equal to 22 percent, available phosphorus (P)2O5) Not less than 12%, the percentage of water-soluble phosphorus in phosphorus is not less than 50%, and potassium chloride (K)2O) content is more than or equal to 8 percent, moisture (free water) is less than or equal to 2.2 percent, average compression strength N of the particles is more than or equal to 12 percent, and the particle size (1.0-4.75mm) is more than or equal to 85 percent.

Claims (2)

1. The production process of the disposable multi-element compound fertilizer is characterized in that: the nitrogen-phosphorus-potassium compound fertilizer is produced by using bentonite, triple superphosphate, potassium chloride and urea in the weight ratio of 1 to 6.43 to 2.87 to 8.7, and through pelletizing, drying and cooling on the basis of using sulfuric acid and liquid ammonia as reaction heat.
2. The production process according to claim 1, characterized in that:
(1) evenly mixing bentonite, heavy calcium, potassium chloride and urea in a weight ratio of 1: 6.43: 2.87: 8.7;
(2) modifying the coarse whiting by adopting an amino-transfer method, introducing liquid ammonia (containing 82.3 percent of nitrogen) at araw material inlet of a granulator, adding the liquid ammonia according to 1.35 percent of the amount of a finished product, and carrying out ammoniation treatment on the coarse whiting in the raw material;
(3) heating the materials in the granulating bed layer by adopting ammonia-acid reaction heat, and adding liquid ammonia and sulfuric acid into the granulating section at the same time according to the weight ratio of 1: 2-3.5;
(4) in the reaction process of the ammonia and the acid, the temperature of the material at the outlet of the granulator is ensured to be between 60 and 80 ℃, the PH value is between 5.5 and 7.0, and the water content is less than or equal to 3.0 percent;
(5) the material at the outlet of the granulator is sent into a dryer for drying, the temperature at the inlet of the dryer is between 110 and 165 ℃, and the temperature of the material at the inlet of the dryer is ensured to be between 60 and 70 ℃, and the moisture content is less than or equal to 2.0 percent;
(6) and (3) feeding the material at the outlet of the granulator into a cooling machine for cooling treatment, and ensuring that the temperature of the material is reduced to 35-55 ℃.
CN98114356A 1998-09-25 1998-09-25 Prodn. tech. of disposable multi-element compound fertilizer Expired - Fee Related CN1088446C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN98114356A CN1088446C (en) 1998-09-25 1998-09-25 Prodn. tech. of disposable multi-element compound fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN98114356A CN1088446C (en) 1998-09-25 1998-09-25 Prodn. tech. of disposable multi-element compound fertilizer

Publications (2)

Publication Number Publication Date
CN1221719A true CN1221719A (en) 1999-07-07
CN1088446C CN1088446C (en) 2002-07-31

Family

ID=5224026

Family Applications (1)

Application Number Title Priority Date Filing Date
CN98114356A Expired - Fee Related CN1088446C (en) 1998-09-25 1998-09-25 Prodn. tech. of disposable multi-element compound fertilizer

Country Status (1)

Country Link
CN (1) CN1088446C (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101792354A (en) * 2010-04-07 2010-08-04 中盐安徽红四方股份有限公司 Color drought-resistance water-retention sustained-release compound fertilizer and method for producing same
CN101391934B (en) * 2008-10-24 2010-12-01 江苏阿波罗复合肥有限公司 Ammoniation granulator and composite fertilizer production novel technique
CN101284743B (en) * 2007-04-10 2012-02-22 上海化工研究院 Process for preparing complex fertilizer using sulfuric acid and ammine as partial raw material
CN102417427A (en) * 2011-09-08 2012-04-18 河南心连心化肥有限公司 Polyaspartic acid slow release compound fertilizer and production method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1089932A (en) * 1993-01-19 1994-07-27 上海青浦化工厂 Granulated ammonium bicarbonate complex mixed fertilizer production method
CN1115749A (en) * 1994-07-26 1996-01-31 湖南省郴州地区化肥厂 Prodn process of ternary compound fertilizer with KCl

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101284743B (en) * 2007-04-10 2012-02-22 上海化工研究院 Process for preparing complex fertilizer using sulfuric acid and ammine as partial raw material
CN101391934B (en) * 2008-10-24 2010-12-01 江苏阿波罗复合肥有限公司 Ammoniation granulator and composite fertilizer production novel technique
CN101792354A (en) * 2010-04-07 2010-08-04 中盐安徽红四方股份有限公司 Color drought-resistance water-retention sustained-release compound fertilizer and method for producing same
CN101792354B (en) * 2010-04-07 2013-07-10 中盐安徽红四方股份有限公司 Color drought-resistance water-retention sustained-release compound fertilizer and method for producing same
CN102417427A (en) * 2011-09-08 2012-04-18 河南心连心化肥有限公司 Polyaspartic acid slow release compound fertilizer and production method thereof

Also Published As

Publication number Publication date
CN1088446C (en) 2002-07-31

Similar Documents

Publication Publication Date Title
CN1210230C (en) Processes for preparing granular composite fertilizer compositions and products produced thereby
CA2506093A1 (en) A process for the manufacture of sulphur-containing ammonium phosphate fertilizers
CN102153424B (en) Novel method for preparing humic acid urea slow release fertilizer
CN1880286A (en) Complex fertilizer production method without drying process
CN102633553B (en) Method for producing high-tower ammonium phosphate compound fertilizer
KR101850524B1 (en) Method for producing fertilizers containing dispersed micronized sulphur
CN1187116C (en) Process for preparing granular fertilizer
CN114890835A (en) Preparation method of modified poly-humic acid ammonium phosphate
CN101041603A (en) Preparation technical method of urine sulfur radical composite fertilizer
CN1088446C (en) Prodn. tech. of disposable multi-element compound fertilizer
CN1280968A (en) Process for preparing organic composite N-P-K fertilizer from solidified substance in black paper-making liquid
CN1024274C (en) Compound fertilizer by spray granulating and preparation thereof
CN1208288C (en) Drum peletizing process of molten ammonium nitrate-urea slurry to produce granulated composite fertilizer
CN1022620C (en) Large-granule, long-acting fetilizer
CN85101008A (en) Wrapped fertilizer and manufacturing process thereof
CN1062846C (en) Technology for production of modified calcium superphosphate compounded fertilizer
FI105472B (en) Multi-suspension process for the preparation of a fertilizer
EP4166526A1 (en) Method for producing a potassium-containing fertilizer with a low content of water-insoluble material
EP1480926A2 (en) Method for producing granular fertilisers
CN1267383C (en) Pelleting process for composite manure
CN1453248A (en) High-nitrogen urine-based medium-concentration composite fertilizer and its production process
CN1297869A (en) Method of producing ternary composite azophoska
RU2221758C1 (en) Mixed nitrogen-phosphorus fertilizer and a method for production thereof
JPS6048478B2 (en) Manufacturing method of modified dissolved phosphorus fertilizer
CN1364750A (en) Slurry-spraying pelletizing process for producing potassium sulfate compound fertilizer using calcium superphosphate as phosphor source

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee